Preparation and use of tetrasubstituted fluorenyl catalysts for polymerization of olefins

ABSTRACT

Catalyst compositions and processes for the polymerization of ethylenically unsaturated monomers to produce polymers, including copolymers or homopolymers. The polymerization catalyst characterized by the formula B(FluL)MQ n  in which Flu is a fluorenyl group substituted at least the 2,7- and 3,6-positions by hydrocarbyl groups. L is a substituted or unsubstituted cyclopentadienyl, indenyl or fluorenyl group or a heteroorgano group, XR, in which X is a heteroatom from Group 15 or 16 of the Periodic Table of Elements, R is an alkyl group, a cycloalkyl group or an aryl group and B is a structural bridge extending between the groups L and Flu, M is a Group 4 or Group 5 transition metal, such as titanium, zirconium or hafnium and Q is selected from the group consisting of chlorine, bromine, iodine, an alkyl group, an amino group, an aromatic group and mixtures thereof, with n being 1 or 2.

FIELD OF THE INVENTION

This invention relates to olefin polymerization catalysts and their usein the polymerization of ethylenically unsaturated monomers.

BACKGROUND OF THE INVENTION

Olefin polymers such as polyethylene, polypropylene, which may beatactic or stereospecific, such as isotactic or syndiotactic, andethylene-higher alpha olefin copolymers, such as ethylene-propylenecopolymers can be produced under various polymerization conditions andemploying various polymerization catalysts. Such polymerizationcatalysts include Ziegler-Natta catalysts and non-Ziegler-Nattacatalysts, such as metallocenes and other transition metal catalystswhich are typically employed in conjunction with one or moreco-catalysts. The polymerization catalysts may be supported orunsupported.

The alpha olefin homopolymers or copolymers may be produced undervarious conditions in polymerization reactors which may be batch typereactors or continuous reactors. Continuous polymerization reactorstypically take the form of loop-type reactors in which the monomerstream is continuously introduced and a polymer product is continuouslywithdrawn. For example, polymers such as polypropylene, polyethylene orethylene-propylene copolymers involve the introduction of the monomerstream into the continuous loop-type reactor along with an appropriatecatalyst system to produce the desired olefin homopolymer or copolymer.The resulting polymer is withdrawn from the loop-type reactor in theform of a “fluff” which is then processed to produce the polymer as araw material in particulate form as pellets or granules. In the case ofC₃₊ alpha olefins, such a propylene or substituted ethylenicallyunsaturated monomers such as styrene or vinyl chloride, the resultingpolymer product may be characterized in terms of stereoregularity, suchas in the case of, for example, isotactic polypropylene or syndiotacticpolypropylene.

The structure of isotactic polypropylene can be described as one havingthe methyl groups attached to the tertiary carbon atoms of successivemonomeric units falling on the same side of a hypothetical plane throughthe main chain of the polymer, e.g., the methyl groups are all above orbelow the plane. Using the Fischer projection formula, thestereochemical sequence of isotactic polypropylene is described asfollows:

In Formula 1, each vertical segment indicates a methyl group on the sameside of the polymer backbone. Another way of describing the structure isthrough the use of NMR. Bovey's NMR nomenclature for an isotactic pentadas shown above is . . . mmmm . . . with each “m” representing a “meso”dyad, or successive pairs of methyl groups on the same said of the planeof the polymer chain. As is known in the art, any deviation or inversionin the structure of the chain lowers the degree of isotacticity andcrystallinity of the polymer.

In contrast to the isotactic structure, syndiotactic propylene polymersare those in which the methyl groups attached to the tertiary carbonatoms of successive monomeric units in the chain lie on alternate sidesof the plane of the polymer. Syndiotactic polypropylene using the Fisherprojection formula can be indicated by racemic dyads with thesyndiotactic pentad rrrr shown as follows:

Here, the vertical segments again indicate methyl groups in the case ofsyndiotactic polypropylene, or other terminal groups, e.g. chloride, inthe case of syndiotactic polyvinyl chloride, or phenyl groups in thecase of syndiotactic polystyrene.

Other unsaturated hydrocarbons which can be polymerized or copolymerizedwith relatively short chain alpha olefins, such as ethylene andpropylene include dienes, such as 1,3-butadiene or 1,4-hexadiene oracetylenically unsaturated compounds, such as methylacetylene.

SUMMARY OF THE INVENTION

In accordance with the present invention, there are provided catalystcompositions and processes for the polymerization of ethylenicallyunsaturated monomers to produce polymers, including copolymers orhomopolymers. Monomers, which are polymerized or copolymerized inaccordance with the present invention, include ethylene, C₃₊ alphaolefins and substituted vinyl compounds, such as styrene and vinylchloride. A particularly preferred application of the invention is inthe polymerization of propylene including the homopolymerization ofpropylene to produce polypropylene, preferably isotactic polypropyleneand syndiotactic polypropylene having a high melting temperature, andthe copolymerization of ethylene and a C₃₊ alpha olefin to produce anethylene alpha olefin copolymer, specifically an ethylene-propylenecopolymer.

In carrying out the present invention, there is provided an olefinpolymerization catalyst characterized by the formula:

B(FluL)MQ_(n)  (3)

In formula (3), Flu is a fluorenyl group substituted at least the 2,7-and 3,6-positions by hydrocarbyl groups, preferably relatively bulkyhydrocarbyl groups. L is a substituted or unsubstitutedcyclopentadienyl, indenyl or fluorenyl group or a heteroorgano group,XR, in which X is a heteroatom from Group 15 or 16 of the Periodic Tableof Elements, and R is an alkyl group, a cycloalkyl group or an arylgroup. Preferably X is nitrogen, phosphorus, oxygen or sulfur. Morepreferably, X will take the form of nitrogen. R is an alkyl group orcycloalkyl group containing from 1 to 20 carbon atoms, or a mononucleararomatic group which may be substituted or unsubstituted. Further, withrespect to formula (3), B is a structural bridge extending between thegroups L and Flu, which imparts stereorigidity to the ligand structure.Preferably, the bridge B is characterized by the formula ER¹R², in whichE is a carbon, silicon or germanium atom, and R¹ and R² are eachindependently a hydrogen, a C₁-C₁₀ alkyl group, an aromatic group or acycloalkyl group. Further, with respect to formula (3), M is a Group 4or Group 5 transition metal, preferably titanium, zirconium or hafnium.Q is selected from the group consisting of chlorine, bromine, iodine, analkyl group, an amino group, an aromatic group and mixtures thereof, nis 1 or 2 and will have a value of 2 where the transition metal iszirconium, hafnium or titanium.

In one embodiment of the invention, the fluorenyl group Flu issubstituted with an aryl group at each of the 2- and 7-positions andwith a lower molecular weight substituent at each of the 3- and6-positions. More specifically, the fluorenyl group is substituted atthe 2- and 7-positions with a phenyl or substituted phenyl group and ateach of the 3- and 6-positions with a bulky hydrocarbyl group containingat least 4 carbon atoms. Preferably, the bulky hydrocarbyl group at the3- and 6-positions is a tertiary butyl group.

In the embodiment of the invention in which the metallocene component issubstituted at the 2- and 7-positions with an aryl group as describedabove and at the 3- and 6-positions with a tertiary butyl group, themetallocene component is characterized by the formula:

wherein Ar is a phenyl group or substituted phenyl group.

In a specific embodiment of the invention in which the ligand componentL is a heteroorgano group, the metallocene component is characterized bythe formula:

wherein Ar is a phenyl group or a substituted phenyl group, and R is analkyl group having from 1 to 20 carbon atoms or an aryl group havingfrom 6 to 20 carbon atoms.

In a further embodiment of the invention in which the metallocenecomponent incorporates a cyclopentadienyl group, the metallocene ischaracterized by the formula:

In formula (6), Ar is a phenyl group or substituted phenyl group, R′ isa C₁-C₄ alkyl group or an aryl group, n is the number of substituents,from 0 to 4, E is a —C— group or an —Si— group, R¹ and R² are eachindependently a hydrogen, a C₁-C₁₀ alkyl group, or a cycloalkyl group,or an aryl group, M is titanium, zirconium or hafnium, and Q ischlorine, a methyl group or a phenyl group. Preferably, in formula (6),the cyclopentadienyl group is unsubstituted, disubstituted ortetra-substituted to provide a metallocene component which exhibitsbilateral symmetry. In another embodiment of the invention, however, thecyclopentadienyl group is monosubstituted or trisubstituted to provide ametallocene component which exhibits non-bilateral symmetry.

In yet a further embodiment of the invention, the metallocene componentincorporates a cyclopentadienyl group which is substituted with a methylgroup and a tertiary butyl group to provide a metallocene componentcharacterized by the formula:

In formula (7), Ar is a phenyl group or substituted phenyl group, E is a—C— group or an —Si— group, R¹ and R² are each independently a hydrogen,a C₁-C₁₀ alkyl group, or a cycloalkyl group, or an aryl group, M istitanium, zirconium or hafnium, and Q is chlorine, a methyl group or aphenyl group.

In yet a further embodiment of the invention, the metallocene componentincorporates an unsubstituted cyclopentadienyl group and ischaracterized by the formula:

In formula (8), Ar is a phenyl group or substituted phenyl group, R¹ andR² are each independently a hydrogen, a C₁-C₁₀ alkyl group, or acycloalkyl group, or an aryl group, E is a —C— group or an —Si— group, Mis titanium, zirconium or hafnium, and Q is chlorine, a methyl group ora phenyl group.

Another embodiment of the invention involves a metallocene catalystcomponent which incorporates an indenyl group and is characterized bythe formula:

In formula (9), Ar is a phenyl group or substituted phenyl group, Ind isan indenyl or substituted indenyl group, E is a —C— group or an —Si—group, each of R¹ and R² is a C₁-C₄ alkyl group, M is titanium,zirconium or hafnium, and Q is chlorine, a methyl group or a phenylgroup. In this aspect of the invention, the indenyl group may be atetrahydroindenyl group which is substituted or unsubstituted.

In another aspect of the invention in which the secondary ligandcomponent L is a fluorenyl group, the metallocene component ischaracterized by the formula:

In formula (10), Flu′ is a fluorenyl or a substituted fluorenyl group, Eis a —C— group or an —Si— group, each of R¹ and R² is a C₁-C₄ alkylgroup, M is titanium, zirconium or hafnium, and Q is chlorine, a methylgroup or a phenyl group. Preferably, the fluorenyl group Flu′ in formula(10) is an unsubstituted fluorenyl group or a substituted fluorenylgroup wherein the metallocene component exhibits bilateral symmetry.

In yet a further aspect of the invention, there is provided a processfor the polymerization of one or more ethylenically unsaturated monomersto produce a corresponding homopolymer or copolymer. In carrying out thepolymerization process, there is provided a metallocene catalystcomponent as characterized by the above formula (3). In addition to themetallocene catalyst component, there is provided an activatingcocatalyst component. The catalyst component and the cocatalystcomponent are contacted in a polymerization reaction zone with anethylenically unsaturated monomer under polymerization conditions toproduce a polymer product which is then recovered from the reactionzone. Preferably, the activating co-catalyst comprises methylalumoxane(MAO) or tri-isobutylalumoxane (TIBAO) or mixtures thereof.Alternatively, the activating co-catalyst can take the form of anoncoordinating anionic type, such as triphenylcarbeniumtetrakis(pentafluorophenyl)aluminate or triphenylcarbeniumtetrakis(pentafluorophenyl)boronate. Preferably, the ethylenicallyunsaturated monomer is a C₃₊ alpha olefin. More specifically, the alphaolefin is propylene and the polymerization reaction is carried out toproduce syndiotactic or isotactic polypropylene.

In a preferred embodiment of the invention, the metallocene componentincorporates a cyclopentadienyl group and is characterized by theformula:

In formula (II), Ar is a phenyl group or substituted phenyl group, R¹and R² are each independently a hydrogen, a C₁-C₁₀ alkyl group, or acycloalkyl group, or an aryl group, R′ is a C₁-C₄ alkyl group or an arylgroup, n is a number from 0 to 4, E is a —C— group or an —Si— group,each of R₁ and R₂ is a C₁-C₄ alkyl group, M is titanium, zirconium orhafnium, and Q is chlorine, a methyl group, a phenyl group, or asubstituted phenyl or benzyl group. In one aspect of this embodiment ofthe invention, the metallocene component exhibits bilateral symmetry andthe polymer product is syndiotactic polypropylene. In another aspect,the metallocene does not exhibit bilateral symmetry and the polymerproduct is isotactic polypropylene. In a specific embodiment of theprocess, the metallocene component incorporates an unsubstitutedcyclopentadienyl group and is characterized by the formula:

to produce a syndiotactic polypropylene having a melting temperaturehigher than 150° C. and a crystallization temperature of more than 95°C. Preferably, the syndiotactic polypropylene has a melting temperaturegreater than 170° C.

DETAILED DESCRIPTION OF INVENTION

The present invention involves bridged transition metal catalysts havingmetallocene ligand structures incorporating tetra-substituted fluorenylgroups and their use in the polymerization of olefins. Specific olefinswhich may be polymerized, either through homopolymerization orcopolymerization include ethylene, propylene, butylene, as well asmonoaromatic or substituted vinyl compounds as described previously. Thebridged catalyst components of the present invention incorporatetransition metals from Groups 4 or 5 of the Periodic Table of Elements(new notation) and more particularly, transition metals from Group 4 ofthe Periodic Table of Elements. Preferred transition metals for use inthe catalyst components of the present invention are titanium, zirconiumand hafnium, with zirconium being particularly preferred.

The catalyst components of the present invention incorporate a primaryfluorenyl group that is tetra-substituted fluorenyl group which isbridged to a secondary ligand structure which is a substituted orunsubstituted cyclopentadienyl, indenyl or fluorenyl group or aheteroorgano group. The tetra-substituted fluorenyl groups aresymmetrical with respect to a plane of symmetry through the bridge andthe transition metal. Preferably, the substituents at the 2,7 positionsare bulkier than the substituents at the 3,6 positions. However, areverse relationship of substitution may be employed in some instances.In this case, the primary fluorenyl group may be substituted at the 2-and 7-positions with a C₁-C₃ alkyl group and at the 3- and 6-positionswith a bulky hydrocarbyl group containing at least 4 carbon atoms. Morespecifically, the catalyst components of the present invention comprisemetallocene ligand structures which incorporate tetra-substitutedfluorenyl groups substituted at least the 2,7 and 3,6 positions whichare bridged to substituted or unsubstituted cyclopentadienyl, indenyl,fluorenyl or heteroorgano groups and which are characterized in terms ofsymmetry (or asymmetry) with reference to a plane of symmetry extendingthrough the bridge and the transition metal.

The following diagrams indicate metallocene ligand structures (and thenumbering schemes for such structures) which may be employed in carryingout the present invention. Diagram (13) indicates acyclopentadienyl-fluorenyl ligand structure, diagram (14) anindenyl-fluorenyl ligand structure, diagram (15) a heteroatom(XR)-fluorenyl ligand structure, and diagram (16) a fluorenyl-fluorenylligand structure.

The numbering schemes used to indicate the position of substituents onthe various ligand structures are indicated on diagrams (13)-(16). Withrespect to structure (14), while not shown, the indenyl moiety may takethe form of 4,5,6,7-tetrahydro indenyl as well as the more commonunhydrogenated indenyl group. For each of diagrams (13)-(16), themetallocene ligand structures may be characterized in terms of a planeof symmetry extending perpendicular to the plane of the paper throughthe bridge group B and the transition metal (not shown) in diagrams(13)-(16) which would project upwardly from the plane of the paper.

As described with respect to various examples given below and withrespect, for example, to diagram (13), the cyclopentadienyl group may bemonosubstituted and the fluorenyl group may be symmetrically substitutedat the 2,7 and 3,6 positions. If there are no other substituents or ifthe fluorenyl group is otherwise symmetrically substituted, the3-position is equivalent to the 4-position on the cyclopentadienyl groupand this relationship may be expressed by the positional expression3(4).

The catalysts of the present invention can be advantageously used inpropylene polymerization to produce syndiotactic or isotacticpolypropylenes with high yields, having high molecular weights, hightacticities and high melt temperatures. Desired features of thecatalysts of the present invention are due to a unique combination ofstructural parameters of the catalysts and substitutions of thecyclopentadienyl and fluorenyl rings. In addition, the catalysts of thepresent invention can be used in copolymerization of propylene witholefins, e.g. ethylene to yield random or impact copolymers.

Ligand structures suitable for use in carrying out the present inventionwhich can be employed to produce isotactic polypropylene include, withreference to diagram (13), 3-tertiary butyl, 5-methyl cyclopentadienyl,2,7-ditertiary butyl, 4-phenyl fluorene, the same ligand structureexcept with substitution on the fluorenyl structure at the 5-positionand the same ligand structure with substitution at the 4- or 5-positionsby a 4-tertiary butyl phenyl group. In other words, the phenyl group issubstituted by a tertiary butyl group at the directly distal positionwith respect to the substitution of the phenyl group on the fluorenylgroup.

Other suitable ligand structures which can be employed to produceisotactic polypropylene include ligand structures such as describedabove, except the cyclopentadienyl group is mono-substituted at the3-position with a tertiary butyl group. The fluorenyl group issubstituted as before at the 2- and 7-positions with the tertiary butylgroups and at the 4-position with a phenyl group or a 4-tertiary butylphenyl group.

Similarly substituted ligand structures may be employed in accordancewith the present invention incorporating a bis-indenyl fluorenyl ligandstructure exemplified by diagram (14). Typically, because of theunbalanced characteristic of the indenyl structure, further substitutionof the indenyl (or the 4,5,6,7-tetrahyrdo indenyl) group will not beemployed. The fluorenyl ligand component may be substituted as describedpreviously, thus, it may be substituted at the 4-position ordi-substituted at the 4- and 5-positions with bulky groups such astertiary butyl and phenyl groups. Also, the fluorenyl ligand structuremay be substituted at one of the 4- and 5-positions and disubstituted atthe 2- and 7-positions with substituent groups which are less bulky thanthe substituents on the 4- or 5-positions.

The heteroatom ligand structure depicted in diagram (15) may besubstituted on the fluorenyl group similarly as described above withrespect to diagrams (13) and (14). Thus, for example, the fluorenylgroup may be substituted at the 2- and 7-positions with tertiary butylgroups and substituted at the 4-position with a substituted orunsubstituted phenyl group. Alternatively, the fluorenyl group may beunsubstituted at the 2- and 7-positions and substituted at the4-position with an isopropyl group, a tert-butyl group, a phenyl groupor a substituted phenyl group.

In employing the catalyst components of the present invention inpolymerization procedures, they are used in conjunction with anactivating co-catalyst. Suitable activating co-catalysts may take theform of co-catalysts such are commonly employed in metallocene-catalyzedpolymerization reactions. Thus, the activating co-catalyst may take theform of an aluminum co-catalyst. Alumoxane co-catalysts are alsoreferred to as aluminoxane or polyhydrocarbyl aluminum oxides. Suchcompounds include oligomerie or polymeric compounds having repeatingunits of the formula:

where R is an alkyl group generally having 1 to 5 carbon atoms.Alumoxanes are well known in the art and are generally prepared byreacting an organo-aluminum compound with water, although othersynthetic routes are known to those skilled in the art. Alumoxanes maybe either linear polymers or they may be cyclic, as disclosed forexample in U.S. Pat. No. 4,404,344. Thus, alumoxane is an oligomeric orpolymeric aluminum oxy compound containing chains of alternatingaluminum and oxygen atoms whereby the aluminum carries a substituent,preferably an alkyl group. The structure of linear and cyclic alumoxanesis generally believed to be represented by the general formula—(Al(R)—O-)-m for a cyclic alumoxane, and R²Al—O—(Al(R)—O)m-AlR² for alinear compound wherein R independently each occurrence is a C₁-C₁₀hydrocarbyl, preferably alkyl or halide and m is an integer ranging from1 to about 50, preferably at least about 4. Alumoxanes also exist in theconfiguration of cage or cluster compounds. Alumoxanes are typically thereaction products of water and an aluminum alkyl, which in addition toan alkyl group may contain halide or alkoxide groups. Reacting severaldifferent aluminum alkyl compounds, such as, for example,trimethylaluminum and tri-isobutylaluminum, with water yields so-calledmodified or mixed alumoxanes. Preferred alumoxanes are methylalumoxaneand methylalumoxane modified with minor amounts of other higher alkylgroups such as isobutyl. Alumoxanes generally contain minor tosubstantial amounts of the starting aluminum alkyl compounds. Thepreferred co-catalyst, prepared either from trimethylaluminum ortri-isobutylaluminum, is sometimes referred to as poly (methylaluminumoxide) and poly (isobutylaluminum oxide), respectively.

The alkyl alumoxane co-catalyst and transition metal catalyst componentare employed in any suitable amounts to provide an olefin polymerizationcatalyst. Suitable aluminum transition metal mole ratios are within therange of 10:1 to 20,000:1 and preferably within the range of 100:1 to5,000:1. Normally, the transition metal catalyst component and thealumoxane, or other activating co-catalyst as described below, are mixedprior to introduction in the polymerization reactor in a mode ofoperation such as described in U.S. Pat. No. 4,767,735 to Ewen et al.The polymerization process may be carried out in either a batch-type,continuous or semi-continuous procedure, but preferably polymerizationof the olefin monomer (or monomers) will be carried out in a loop typereactor of the type disclosed in the aforementioned U.S. Pat. No.4,767,735. Typical loop type reactors include single loop reactors orso-called double loop reactors in which the polymerization procedure iscarried in two sequentially connected loop reactors. As described in theEwen et al. patent, when the catalyst components are formulatedtogether, they may be supplied to a linear tubular pre-polymerizationreactor where they are contacted for a relatively short time with thepre-polymerization monomer (or monomers) prior to being introduced intothe main loop type reactors. Suitable contact times for mixtures of thevarious catalyst components prior to introduction into the main reactormay be within the range of a few seconds to 2 days. For a furtherdescription of suitable continuous polymerization processes which may beemployed in carrying out the present invention, reference is made to theaforementioned U.S. Pat. No. 4,767,735, the entire disclosure of whichis incorporated herein by reference,

Other suitable activating co-catalysts which can be used in carrying outthe invention include those catalysts which function to form a catalystcation with an anion comprising one or more boron atoms. By way ofexample, the activating co-catalyst may take the form oftriphenylcarbenium tetrakis(pentafluorophenyl) boronate as disclosed inU.S. Pat. No. 5,155,080 to Elder et al. As described there, theactivating co-catalyst produces an anion which functions as astabilizing anion in a transition metal catalyst system. Suitablenoncoordinating anions include [W(PhF₅)]⁻, [Mo(PhF₅)]⁻ (wherein PhF₅ ispentafluorophenyl), [ClO₄]⁻, [S₂O₆]⁻, [PF₆]⁻, [SbR₆]⁻, [AlR₄]⁻ (whereineach R is independently Cl, a C₁-C₅ alkyl group preferably a methylgroup, an aryl group, e.g. a phenyl or substituted phenyl group, or afluorinated aryl group). Following the procedure described in the Elderet al. patent, triphenylcarbenium tetrakis(pentafluorophenyl) boronatemay be reacted with pyridinyl-linked bis-amino ligand of the presentinvention in a solvent, such as toluene, to produce a coordinatingcationic-anionic complex. For a further description of such activatingco-catalyst, reference is made to the aforementioned U.S. Pat. No.5,155,080, the entire disclosure of which is incorporated herein byreference.

In addition to the use of an activating co-catalyst, the polymerizationreaction may be carried out in the presence of a scavenging agent orpolymerization co-catalyst which is added to the polymerization reactoralong with the catalyst component and activating co-catalyst. Thesescavengers can be generally characterized as organometallic compounds ofmetals of Groups 1A, 2A, and 3B of the Periodic Table of Elements. As apractical matter, organoaluminum compounds are normally used asco-catalysts in polymerization reactions. Specific examples includetriethylaluminum, tri-isobutylaluminum, diethylaluminum chloride,diethylaluminum hydride and the like. Co-catalysts normally employed inthe invention include methylalumoxane (MAO), triethylaluminum (TEAL) andtri-isobutylaluminum (TIBAL).

The bridged fluorenyl ligand structures and the corresponding transitionmetal catalyst components can be prepared by any suitable techniques.Typically, for methylene bridged cyclopentadienyl fluorenyl ligandstructures, the fluorenyl group is treated with methyl lithium to resultin a fluorenyl group substituted with lithium in the 9-position and thisis then reacted with a 6,6-substituted fulvene. For example,6,6-dimethyl fulvene may be employed to produce the isopropylidenecyclopentadienyl substituted fluorenyl ligand structure. For a ligandstructure in which the bridge group incorporates a germanium or siliconatom, the lithiumated fluorenyl group is reacted, for example, withdiphenylsilyl dichloride to produce the diphenylsilyl chloridesubstituent at the 9-position on the fluorenyl group. This component isthen reacted with the lithiumated cyclopentadienyl or substitutedcyclopentadienyl to produce the bridge. The ligand structure is thentreated with methyl lithium, followed by reaction with the appropriatetransition metal, chlorine, e.g. zirconium tetrachloride, to produce thecorresponding metallocene dichloride.

The catalyst components employed in the present invention can beprepared by techniques, which include procedures well-known in the artwith appropriate modification of the fluorenyl ligand component toincorporate a 2,7,3,6-tetra-substituted fluorene. For example, asdescribed below, 6,6-dimethyl fulvene can be employed in conjunctionwith 2,7,3,6 symmetrically substituted fluorene in order to produce thecorresponding methylene-bridged cyclopentadienyl2,7,3,6-tetra-substituted fluorene. The fluorenyl-fluorenyl ligandstructures employed in the present invention can be synthesized using aprocedure such as disclosed in U.S. Pat. No. 6,313,242 to Reddy to formbis-fluorenyl ligands, again with the qualification that a symmetricalligand structure rather than the staggered ligand structure of the typedisclosed in Reddy will be produced. Similarly, a bridged fluorenylheteroatom ligand structure of the type characterized by formula 10above can be produced by preparation of a substituted fluorene withdimethyldichlorosilane, followed by reaction with a tertiarybutyllithiumamide to produce the bridged fluorenyl amine structure.Again, the above procedure would be followed, but with the modificationto employ, for example, 2,7-diphenyl,3,6-ditertiary butyl fluorenerather than the 3,6-ditertiary butyl fluorene disclosed in the Reddypatent. The various procedures which can be used in the synthesis of themetallocene components of the present invention are illustrated by thesynthesis procedures described below.

Specific metallocenes embodying the present invention are illustrated bythe following structural formulas in which the isopropylidene bridgegroup is illustrated by X and a tertiary butyl group is indicated by

1. Synthesis of Catalysts

2,7-Dibromo-3,6-di-t-butyl-fluorene was synthesized by the reaction of3,6-di-t-butyl-fluorene with N-bromo succinimide in propylene carbonatesolution in 82% yield in accordance with the following reaction and usedas a starting material for the synthesis of2,7-di-aryl-3,6-di-tert-butyl-fluorenes for catalysts M1-M15:

The coupling reaction of 2,7-dibromo-3,6-di-t-butyl-fluorene with phenylboronic acid provided 2,7-phenyl-3,6-di-t-butyl-fluorene in 90% yield inaccordance with the following reaction:

Example 1 Synthesis of 2,7-Dibromo-3,6-di-t-butyl-fluorene

To a solution of 3,6-di-t-butylfluorene (2.10 g, 7.55 mmol) in propylenecarbonate (60 ml) was added 2.70 g of N-bmmosuccinimide. The reactionmixture was stirred for 6 hours at 70-75° C. The mixture was poured intowater and the precipitated solid was filtered, washed with water anddried to produce a yield of 2.71 g (82%). ¹H NMR (CDCl₃): δ 7.80 and7.72 (each s, 2H, 1,8- and 4,5-H (Flu), 3.74 (s, 2H, H9), 1.59 (s, 18H,t-Bu).

The coupling reaction of 2,7-dibromo-3,6-di-t-butyl-fluorene with arylboronic acid produced 2,7-aryl-3,6-di-t-butyl-fluorene in an 85-95%yield in accordance with the following reaction:

Example 2 Synthesis of 2,7-Diphenyl-3,6-di-t-butyl-fluorene

To a mixture of 2,7-dibromo-3,6-di-t-butylfluorene (0.96 g, 2.20 mmol)and Pd(PPh₃)₄ (260 mg, 0.22 mmol) in toluene (50 ml) was added asolution of phenylboronic acid (0.81 g, 6.63 mmol) in EtOH (10 ml) and asolution of Na₂CO₃ (1.5 g) in water (10 ml). The reaction mixture wasstirred for 6 hours under reflux. The reaction mixture was quenched withwater, extracted with ether, dried over MgSO₄, and evaporated undervacuum to afford the residue which was purified by column chromatography(silica gel, hexane/CH₂Cl₂=5/1) to produce2,7-diphenyl-3,6-di-t-butyl-fluorene (0.85 g, ˜90%). ¹H NMR (CDCl₃): δ7.96 and 7.15 (each s, 2H, 1,8- and 4,5-H (Flu), 7.33 (m, 10H, Ph), 3.77(s, 2H, H9), 1.27 (s, 18H, t-Bu).

Example 3 Synthesis of2,7-Di(4-tert-butyl-phenyl)-3,6-di-t-butyl-fluorene

The same procedure as in Example 2 was used except4-tert-butyl-phenyl-boronic acid was used in place of phenylboronicacid. The yield was 92%.

The following Examples 4 and 5 illustrate the preparation of2,7-dimethyl-3,6-di-tert-butyl-fluorene.

Example 4 Synthesis of 2,7-dichloromethane-3,6-di-tert-butyl-fluorene

To a solution of 3,6-di-t-butylfluorene (2.00 g, 7.19 mmol) andchloromethyl methyl ether (2.5 ml) in CS₂ (15 ml) was added at 0° C. asolution of TiCl₄ (0.4 ml) in CS₂ (5 ml). The reaction mixture wasstirred for 3 hours at room temperature. The mixture was poured into icewater and extracted with ether. The ether extract was dried over sodiumsulfate and evaporated under vacuum to leave a residue, which waspurified by column chromatography (hexane/CH₂Cl₂=10/1) andcrystallization from hot heptanes. The product provided2-chloromethyl-3,6-di-t-butylfluorene (yield 0.75 g). NMR (CDCl₃): δ7.80 and 7.78 (each d, 1H, 4,5-H), 7.47 (d, 11H, J=8.1 Hz, H8), 7.34(dd, 1H, J=8.1 Hz, J=1.51 Hz, H7), 7.31 (d, 1H, 1H, J=1.5 Hz, H1), 4.72(s, 2H, CH₂Cl), 3.87 (s, 2H, H9), 1.41 (s, 18H, t-Bu) and2,7-dichloromethyl-3,6-di-t-butylfluorene (yield 0.63 g). ¹H NMR(CDCl₃): 7.87 (br s, 2H, 4,5-H), 7.34 (br s, 2H, 1,8-H), 4.75 (s, 4H,CH₂Cl), 3.95 (s, 2H, H9), 1.42 (s, 18H, t-Bu) as indicated by thefollowing reaction:

Example 5 Reduction of 2,7-dichloromethane-3,6-di-tert-butyl-fluorene

To a solution of 2,7-di-chloromethyl-3,6-di-t-butylfluorene (0.75 g) inTHF (15 ml) was added a small portion of LiAlH₄ (0.25 g) under stirring.The mixture was refluxed for 5 hours. The reaction was quenched withwater and NaOH, and extracted with ether. The ether solution wasevaporated under vacuum to produce a white solid with a yield of 0.69 g.

Examples 6 and 7 illustrate the synthesis of2,2-[(cyclopentadienyl)-(2,7-di-phenyl-3,6-di-tert-butylfluorenyl)]-isopropylidenezirconium dichloride (catalyst component M1).

Example 62,2-[(Cyclopentadienyl)1(2,7-di-phenyl-3,6-di-tert-butylfluorenyl)]-propane

Butyllithium (1.5 ml, 1.6M in hexane, 2.40 mmol) was added to2,7-diphenyl-3,6-di-t-butyl-fluorene (0.95 g, 2.20 mmol) in THF (20 ml)at −78° C. The reaction mixture was allowed to warm to room temperatureand stirred for 2.5 hours. The solvent was removed under vacuum. Ether(5 ml) was added and removed under vacuum. Ether (25 ml) was added and6,6′-dimethylfulvene (0.23 g, 2.43 mmol) in ether (5 ml) was added tothe reaction mixture at 0° C. The reaction was stirred at roomtemperature for 5 days. The reaction mixture was quenched with water,extracted with ether, dried over MgSO₄, and evaporated under vacuum toafford the residue which was purified by column chromatography (silicagel, hexane/CH₂Cl₂=5/1) and crystallized from hot hexane. The yield was0.40 g, 34%. ¹H NMR (CDCl₃): δ 7.91 and 7.30 (each s, 2H, 1,8- and 4,5-H(Flu), 7.35 (m, 10H, Ph), 6.76, 6.40 (m, 3H, Cp), 4.04 and 4.02 (s, 2H,H9), 3.00 and 2.78 (br s, 2H, CH2 Cp), 1.31 (s, 18H, t-Bu), 1.11 and1.09 (s, 6H, Me). ¹H NMR (CD₂Cl₂): δ 7.91 and 7.29 (each s, 2H, 1,8- and4,5-H (Flu), 7.2-7.4 (m, 10H, Ph), 6.8-6.7, 6.40 (m, 3H, Cp), 4.02 (brs,2H, H9), 3.00 and 2.78 (br s, 2H, CH₂ Cp), 1.28 (s, 18H, t-Bu), 1.07 and1.04 (s, 6H, Me). HPLC: 10.38 and 10.65 min.

Example 72,2-[(Cyclopentadienyl)-(2,7-di-phenyl-3,6-di-tert-butylfluorenyl)]-propanezirconium dichloride (catalyst M1)

Butyllithium (1.0 ml, 1.6M in Et₂₀, 1.60 mmol) was added to2,2-[(cyclopentadienyl)-[(2,7-di-phenyl-3,6-di-tert-butylfluorenyl)]-propane(0.39 g, 0.73 mmol) in THF (10 ml) at −78° C. The reaction mixture wasallowed to warm to room temperature and stirred for 2.5 hours. Thesolvent was evaporated under vacuum. Ether (5 ml) was added and removedunder vacuum. ZrCl₄ (0.170 g, 0.76 mmol) was added. at −78°. Ether (10ml) was added to reaction mixture. The reaction mixture was allowed towarm to room temperature and stirred for 5 hours. The solvent wasremoved under vacuum to afford an orange solid, which was tested inpropylene polymerization without purification. ¹H NMR (C₆D₆): δ 8.14 (s,2H, Flu-1,8), 7.4-7.2 (m, 12H, Ph, Flu-5,6), 6.04 and 5.69 (each m, 2H,Cp), 1.33 (s, 18H, t-Bu).

Examples 8-10 Illustrate the Synthesis of (4-tert-butyl-phenyl)[(cyclopentadienyl)(2,7-di-phenyl)-(3,6-di-tert-butyl-fluorenyl)]methanezirconium dichloride (catalyst M12). Example 86-(4-tetr-butyl-Phenyl)-5-methyl-3-test-butyl-fulvene

To a solution of methyl-tert-butylcyclopentadiene (4.42 g, 32.5 mmol)and 4-t-butyl-benzaldehyde (5.15 g) in absolute ethanol (30 ml) wasadded a small portions of sodium methoxide (4.0 g) under stirring. Themixture was stirred for 2 hours. The reaction was quenched with waterand extracted with ether. The ether solution was evaporated under vacuumto give an orange liquid, which was purified by column chromatography(silica gel, hexane/CH₂Cl₂=8/1), providing a yield of 7.0 g. ¹H NMR(CDCl₃): δ 7.55 (m, 2H, Ph), 7.48 (m, 2H, Ph), 7.02 (s, 1H, H—CPh), (m,1H, H-6), 6.27 and 6.22 (br s, 2H, H-Cp), 2.18 (s, 3H, Me), 1.39 and1.23 earh (s, 9H, t-Bu).

Example 9(4-tert-butyl-phenyl)[cyclopentadienyl)-[2,7-di-phenyl-3,6-di-tert-butylfluorenyl)]-methane

Butyllithium (1.5 ml, 1.6M in hexane, 2.40 mmol) was added to2,7-diphenyl-3,6-di-t-butyl-fluorene (1.02 g, 2.33 mmol) in ether (20ml) at −78° C. The reaction mixture was allowed to warm to roomtemperature and stirred for 2.5 hours. 6-(4-tert-Butyl-phenyl)-fulvene(0.49 g, 2.33 mmol) in ether (5 ml) was added to the reaction mixture at−20° C. The reaction was stirred at room temperature for 2 hours. Thereaction mixture was quenched with water, extracted with ether, driedover MgSO₄, and evaporated under vacuum to afford the residue, which waswashed with hot ethanol.

Example 10(4-tert-Butyl-phenyl)[(cyclopentadienyl)(2,7-di-phenyl)-(3,6-di-tert-butyl-fluorenyl)]methanezirconium dichloride (catalyst M12)

Butyllithium (1.3 ml, 1.6M, 2.08 mmol) was added to(4-tert-butyl-phenyl)[(cyclopentadienyl)(2,7-di-phenyl)-(3,6-di-tert-butyl-fluorenyl)]methane(0.61 g, 0.95 mmol) in ether (10 ml) at −78° C. The reaction mixture wasallowed to heat to room temperature and the reaction was continued for2.5 hours. The solvent was removed under vacuum. ZrCl₄ (220 mg) wasadded to the reaction mixture. Toluene (15 ml) was added at −20° C. andthe reaction was stirred at room temperature for night. The solvent wasremoved under vacuum.

Catalysts M2-M11 and M13-M18 can be prepared as described in theforegoing Examples through the use of the corresponding2,7-di-substituted-3,6-tert-butyl-fluorene and fulvene.

Examples 11-17 Homogeneous Polymerization with Catalyst M1

The polymerization was conducted in bulk propylene at 40, 60 and 70° C.in a 4 L reactor using the crude catalyst from Reaction 21 withoutpurification. The polymerization behavior for the catalyst is set forthin Tables 1 through 3. The catalyst produced a polymer with activity of30,000 gPP/gcat/h at 60° C. without hydrogen. In the presence ofhydrogen (60 ppm) the activity increased up to 142,400 gPP/gcat/h. Thecatalyst produced syndiotactic polypropylene with pentad rrrr values of85-92% (Table 4), melting temperature of 149-163° C. and molecularweight of 130,000-230,000 (Table 3). A broader molecular weightdistribution (D) was also observed due to the presence of a lowmolecular weight fraction, a content of which could be decreased byfraction extraction of the polymer. Fraction extraction of the samplewith hot hexane for 3 hours provided a polymer with a narrow molecularweight distribution (D=1.9), melting temperature of 153° C. andtacticity of 92% of rrrr pentad.

TABLE 1 Bulk Propylene Polymerization with Unsupported Catalyst M1Activity, Catalyst T, Time, H₂, gPP/g MFR, Example mg ° C. min ppm PP, gcat/h dg/min 11^(a) 20 −10 180 0 2.0 12 7.0 40 60 0 42 6,000 13 10 60 300 150 30,000 3.6 14^(b) 15^(c) 16 5.5 60 10 60 130 142,390 4.3 17 4.3 7030 0 10 4,650 ^(a)Polymerization at 1 atmosphere of propylene in toluene^(b)Crystallized fraction from xylene of sample 13 ^(c)Heptaneextraction of sample 14

TABLE 2 DSC Data of PoIypropylene T melt, T cryst, Delta H Delta HExample ° C. ° C. melt, J/g recryst, J/g 11 163.0 109.0 29.6 −39.3 12160.4 98.6 37.0 −97.9 13 149.4 89.6 46.3 −59.6 14 15 152.7 97.6 44.7−49.0 16 154.4 109.6 40.8 −109.6 17 146.0 101.0 29.2 −48.9

TABLE 3 GPC Data of Polypropylene Example Mn Mw Mz D D′ 11 7,909 222,9221211,160 28^(a) 5.4 12 6,394 169,439 510,047 26.5^(a) 3.0 13 31,719161,604 324,372  5.1 2.0 14 45,600 166,100 338,760  3.6 2.0 15 96,447186,871 335,371  1.9 1.8 16 27,298 149,743 285,755  5.5 1.9 17 26,940129,260 254,190  4.8 2.0 ^(a)bimodal

TABLE 4 Pentad Distributions for Syndiotactic PoIypropylene ExampleExample Example Example Example 12 13 14 16 17 mmmm % 2.1 0.3 0.3 0.40.4 mmmr 4.4 0.6 0.0 0.8 0.5 rmmr 2.5 0.8 0.6 1.0 1.0 mmrr 3.3 1.3 0.91.4 1.5 xmrx 9.2 3.0 1.5 3.2 4.0 mrmr 5.8 1.4 0.0 1.4 0.8 rrrr 65.2 87.592.0 86.3 84.9 rrrm 4.0 3.7 3.8 4.1 5.7 mrrm 3.6 1.4 0.9 1.3 1.2 % meso18.2 4.6 2.1 5.3 5.1 % racemic 81.8 95.4 97.9 94.7 94.9 % error 7.1 2.31.4 2.6 3.0 def/1000° C. 90.9 22.8 10.4 26.5 25.3

Examples 18-25 Homogeneous Polymerization with Catalyst M12

The polymerizations in Examples 18-20 were conducted in bulk propyleneusing 10×-Multi-Clave reactor from Autoclave Engineers in 5 ml of bulkpropylene in 30 ml glass vessels. The catalyst was activated with MAO(Zr/Al=1/1000-2000) prior to polymerization.

TABLE 5 Propylene poIymerization with CataIyst M12 in 10X Multi-CIavereactors (bulk propylene, homogeneous, 60° C., 30 min, no H₂) CatalystActivity, Tmelt, Tcryst, Mw/ Mw/ Mz/ Example (mg) T°, C. Polymer, gg/g//h ° C. ° C. 1000 Mn Mw 18 0.15 50-60 1 13,300 158.7 96.3 206.7 2.61.9 19 0.45 40-50 3.6 10,526 161.9 99.0 278.8 2.9 1.8 20 0.9 20 5.76,333 160.0 96.3 300.0 2.6 1.8 a The highest melting peak

Example 21 Propylene Polymerization Under 1 atm with Catalyst M12

The propylene polymerization in Example 21 was conducted with 1.3 mg ofcatalyst M12, activated with 2 ml of 30% MAO, using the glass reactorunder 1 atm of propylene in toluene solution at −10° C. for 3 hours. 1.6g of polypropylene was isolated. Tmelt=171° C., T cryst=112.3° C.,Mw=446,200, Mw/Mn=3.0, Mz/Mw=1.9.

TABLE 6 Tacticity of polypropylene samples Example Example ExampleTACTICITY, % 20 19 21 mmmm 0.1 0.2 2.5 mmmr 0.3 0.0 1.1 rmmr 0.3 0.2 0.2mmrr 0.6 0.5 0.4 xmrx 0.8 0.4 1.0 mrmr 0.2 0.0 0.1 rrrr 89.7 94.6 90.7rrrm 6.1 3.2 3.0 mrrm 1.9 0.9 1.1 % meso 1.5 0.8 4.5 % racemic 98.5 99.295.5 % error 0.7 0.3 0.7 def/1000 C. 7.4 4.2 22.3

The polymerizations in Examples 22-25 were conducted in bulk propyleneusing a 2 L Zipper-Clave reactor from Autoclave Engineers. The reactorwas charged with 300 g of bulk propylene prior to polymerization. Thecatalyst was activated with MAO (Zr/Al=1/1000-2000) prior topolymerization.

TABLE 7 Bulk propylene polymerization with Catalyst M12 underhomogeneous condition Catalyst T, H2, Activity, MF, Mw/ % Tol Example(mg) ° C. ppm Polymer, g g/g//h Tm, ° C. g/10 min Mw/1000 Mn Mz/Mw Sol22 0.3 50 30 56 373,333 159.7 1.0 219.8 2.6 1.8 0.5 23 0.5 60 60 65260,000 157.7 1.9 173.4 2.2 1.8 0.9 24 0.2 60 30 53 530,000 155.7 1.5176.9 2.2 1.8 25 1.5 70 60 146 195,000 153.4 3.2 154.0 2.5 1.9 0.6As can be seen from Examples 18-25, catalyst M12 produced syndiotacticpolypropylene with pentad rrrr values of 88-95%, melting temperatures of153-171° C., molecular weights of 154,000-300,000 at activities up to530,000 gPP/Gcat/h.

Examples 26-29 Propylene Polymerization Catalyst M1

The catalyst M1 was supported on a silica support available from AsahiGlass Co., Ltd. under the designation H-121. The silica support had anaverage particle size of 12 microns. The catalyst supported on thesilica with a 2 wt. % loading was tested at 60° C. for 1 hour in a 4 Lreactor. The polymerization behavior for the unsupported catalyst is setforth in Tables 8 and 9. The hydrogen response of the supported catalystwas tested. The hydrogen response of the supported catalyst showed thatthe catalyst activity increased as the hydrogen levels increased (Table8). The melting temperature of polymers produced in the presence ofhydrogen was around 136-137° C. and is slightly dependent on hydrogenconcentration. The molecular weight of the polymers showed a range of99,000-78,000 for hydrogen levels of 0-75 ppm. In addition, the meltflow rate slightly increased from 31-44 g/10 min. with increasing thehydrogen concentration from 40 to 75 ppm. The supported catalystproduced a polymer with a narrow molecular weight distribution(D=2.1-2.6). Polymer produced using the supported catalyst showed goodstereoregularity (% rrrr=82-83 in the presence of hydrogen) (Table 9).

TABLE 8 Polymerization Test Results for Supported Catalyst M1 Cat T,Time, H2, Activity, MFR, Example mg ° C. min ppm PP, g gPP/g cat/hdg/min T melt, ° C. Mn Mw Mz D D′ 26 40* 60 60 0 4 100 127.7 38,96799,373 166,385 2.6 1.7 27 40* 60 60 40 25 625 31 137.2/120.9 37,44278,308 129,672 2.1 1.7 28 20* 60 60 60 13 650 39 136.0/119.6 35,64482,217 140,208 2.3 1.7 29 40* 60 60 75 31 775 44 137.2/120.9 37,44278,308 129,672 2.1 1.7

TABLE 9 Pentad Distributions for Syndiotactic Polypropylene Producedwith Supported Catalyst Example 26 Example 27 Example 28 Example 29 mmmm% 0.4 0.1 0.2 0.0 mmmr 0.3 0.2 0.2 0.2 rmmr 1.2 1.3 1.3 1.3 mmrr 2.1 2.12.1 2.2 xmrx 4.6 4.5 4.6 4.3 mrmr 0.4 0.4 0.2 0.3 rrrr 77.9 82.3 82.683.2 rrrm 8.1 7.8 7.9 7.4 mrrm 5.0 1.2 1.1 1.1 % meso 5.4 5.2 5.1 4.9 %racemic 94.6 94.8 94.9 95.1 % error 3.5 3.5 3.6 3.4 def/1000° C. 17.517.7 17.8 17.2

Examples 30-33 Propylene Polymerization with Supported Catalyst M12

The catalyst M12 was supported on silica supports available from AsahiGlass Co., Ltd. under the designation H-121 and G952. The catalystsupported on the silica with a 2 wt. % loading was tested at 60° C. for30 minutes in 500 ml stainless reactor. The results in terms ofpolymerization parameters and polymer properties are shown in Tables 10and 11.

TABLE 10 Propylene polymerization with Supported Catalyst M12 Activity,Tc, Mw/ Mw/ Mz/ Entry # Support Run # H2, ppm Polymer, g g/g/cat/h Tm, °C. ° C. 1000 Mn Mw 30 G952 1137-099-R3 10 6.1 610 142.0/128.3 89.3 1052.5 1.8 31 G952 1137-099-R4 60 7 700 142.4 89.3 96 2.8 1.9 32 H-121-C1137-099-R5 10 1.8 180 139.0 87.3 105 2.7 1.8 33 H-121-C 1137-099-R6 603 300 141.4 86.6 96 2.5 1.8

TABLE 11 Tacticity of poIypropyIene produced with supported Catalyst M12Example 31 Example 33 mmmm, % 0.4 0.4 mmmr 0.3 0.3 rmmr 0.8 0.8 mmrr 1.91.8 xmrx 3.3 3.4 mrmr 0.5 0.0 rrrr 90.4 83.2 rrrm 1.9 8.1 mrrm 0.7 1.8 %meso 4.2 4.2 % racemic 95.8 95.8 % error 2.4 2.6 def/1000° C. 21.2 20.9

Having described specific embodiments of the present invention, it willbe understood that modifications thereof may be suggested to thoseskilled in the art, and it is intended to cover all such modificationsas fall within the scope of the appended claims.

1. A metallocene component for an olefin polymerization catalystcharacterized by the formula:B(FluL)MQ_(n)  (3) wherein: (a) Flu is a fluorenyl group substituted atleast the 2,7 position and the 3,6 position; (b) L is a substituted oran unsubstituted cyclopentadienyl group, a substituted or unsubstitutedindenyl group, a substituted or unsubstituted fluorenyl group, or aheteroorgano group XR2 in which X is a heteroatom from Group 15 or 16 ofthe Periodic Table, and R is an alkyl group, a cycloalkyl group or anaryl group containing from 1 to 20 carbon atoms; (c) B is a structuralbridge between L and Flu imparting stereorigidity to the ligandstructure (FluL); (d) M is a Group 4 or Group 5 transition metal; (e) Qis selected from the group consisting of Cl, Br, I, an alkyl group, anamino group, an aromatic group and mixtures thereof; and (f) n is 1 or2.
 2. The metallocene component of claim 1 wherein the fluorenyl groupFlu is substituted with substituents at the 2,7 positions which arebulkier than the substituents at the 3,6 positions.
 3. The metallocenecomponent of claim 1 wherein the fluorenyl group Flu is substituted withan aryl group at each of the 2 and 7 positions and with a lowermolecular weight substituent at each of the 3 and 6 positions.
 4. Themetallocene component of claim 3 wherein said fluorenyl group Flu issubstituted at each of the 2 and 7 positions with a phenyl or asubstituted phenyl group and at each of the 3 and 6 positions with abulky hydrocarbon group containing at least four carbon atoms.
 5. Thecomponent of claim 4 wherein said fluorenyl group Flu is substituted ateach of the 3 and 6 positions with a tertiary butyl group.
 6. Themetallocene component of claim 1 wherein said fluorenyl group Flu issubstituted at each of the 2 and 7 positions with a C1-C3 alkyl groupand at each of the 3 and 6 positions with a bulky hydrocarbon groupcontaining at least 4 carbon atoms.
 7. The component of claim 5 whereinL is a heteroorgano group, XR2 and wherein X is N, P, O or S, and R isan alkyl, cycloalkyl or aryl group.
 8. The component of claim 7 whereinX is N and R is a mononuclear aromatic group, or an alkyl or cycloalkylgroup containing from 1 to 20 carbon atoms.
 9. The metallocene componentof claim 1 wherein B(FluL)MQn is characterized by the formula:

wherein Ar is a phenyl group or substituted phenyl group.
 10. Themetallocene component of claim 1 wherein B(FluL)MQn is characterized bythe formula:

wherein: Ar is a phenyl group or a substituted phenyl group; and R is analkyl group having from 1 to 20 carbon atoms or an aryl group havingfrom 6 to 20 carbon atoms.
 11. The metallocene component of claim 1wherein B(FluL)MQn incorporates a cyclopentadienyl group and ischaracterized by the formula:

wherein: Ar is a phenyl group or substituted phenyl group; R′ is a C1-C4alkyl group or an aryl group; n is the number of substituents, from 0 to4; E is a —C— group or an —Si— group; R1 and R2 are each independently ahydrogen, a C1-C10 alkyl group, or a cycloalkyl group, or an aryl group;M is titanium, zirconium or hafnium; and Q is chlorine, a methyl groupor a phenyl group.
 12. The metallocene component of claim 11 wherein thecyclopentadienyl group is unsubstituted (n=0), a disubstitutedcyclopentadienyl group (n=2) or a tetrasubstituted cyclopentadienylgroup (n=4) wherein said metallocene component exhibits bilateralsymmetry.
 13. The metallocene component of claim 11 wherein saidcyclopentadienyl group is monosubstituted (n=1) or trisubstituted (n=3)wherein said metallocene component exhibits a non-bilateral symmetry.14. The metallocene component of claim 1 wherein B(FluL)MQn incorporatesa cyclopentadienyl group and is characterized by the formula:

wherein: Ar is a phenyl group or substituted phenyl group; E is a —C—group or an —Si— group; R1 and R2 are each independently a hydrogen, aC1-C10 alkyl group, or a cycloalkyl group, or an aryl group; M istitanium, zirconium or hafnium; and Q is chlorine, a methyl group or aphenyl group.
 15. The metallocene component of claim 1 whereinB(FluL)MQn incorporates a cyclopentadienyl group and is characterized bythe formula:

wherein: Ar is a phenyl group or substituted phenyl group; R1 and R2 areeach independently a hydrogen, a C1-C10 alkyl group, or a cycloalkylgroup, or an aryl group; E is a —C— group or an —Si— group; M istitanium, zirconium or hafnium; and Q is chlorine, a methyl group or aphenyl group.
 16. The metallocene catalyst component of claim 1 whereinB(FluL)MQn incorporates an indenyl group and is further characterized bythe formula:

wherein: Ar is a phenyl group or substituted phenyl group; Ind is anindenyl or substituted indenyl group; E is a —C— group or an —Si— group;each of R1 and R2 is a C1-C4 alkyl group; M is titanium, zirconium orhafnium; and Q is chlorine, a methyl group or a phenyl group.
 17. Themetallocene component of claim 16 wherein said indenyl group is atetrahydroindenyl group which is substituted or unsubstituted.
 18. Themetallocene component of claim 17 wherein said indenyl group is anunsubstituted indenyl group or an unsubstituted tetrahydroindenyl group.19. The metallocene component of claim 1 wherein B(FluL)MQn is furthercharacterized by the formula:

wherein: Flu is a fluorenyl or a substituted fluorenyl group; E is a —C—group or an —Si— group; each of R1 and R2 is a C1-C4 alkyl group; M istitanium, zirconium or hafnium; and Q is chlorine, a methyl group or aphenyl group.
 20. The metallocene component of claim 19 wherein Flu isan unsubstituted fluorenyl group or a substituted fluorenyl groupwherein the metallocene component exhibits bilateral symmetry. 21.(canceled)
 22. (canceled)
 23. (canceled)
 24. (canceled)
 25. (canceled)26. (canceled)
 27. (canceled)
 28. (canceled)
 29. (canceled) 30.(canceled)
 31. (canceled)
 32. (canceled)
 33. (canceled)
 34. (canceled)35. (canceled)